CN102311189B - System for treatment of acid mine drainage and resource recovery of iron, aluminum, copper and zinc in drainage - Google Patents
System for treatment of acid mine drainage and resource recovery of iron, aluminum, copper and zinc in drainage Download PDFInfo
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Abstract
The invention belongs to the field of wastewater treatment and specially, relates to a system for treatment of acid mine drainage and resource recovery of iron, aluminum, copper and zinc in drainage. The system is characterized in that the system is composed of an iron removal system, an aluminum removal system, a copper removal system, a zinc removal system, a sedimentation basin 1 and a sedimentation basin 2 by sequential connection. Based on differences of precipitation performances of a metal ion under pH conditions and differences of solubility products (Ksp) of a reaction between copper and a sulfur-containing organic chelating agent and a reaction between zinc and the sulfur-containing organic chelating agent, through a fractional precipitation method, iron, aluminum, copper, zinc and the like are separated effectively; resource recovery and utilization is realized; hidden troubles of secondary pollution caused by waste residues are eliminated; and treated drainage reaches a reuse standard and can is fed directly into mineral processing pool for reuse. The system has the advantages of simple process, good effect of drainage treatment, stable operation, low costs of treatment, capital construction investment, energy consumption and operation, and wide application prospect.
Description
Technical field
The invention belongs to the waste water treatment field, particularly relate to the resource utilization recovery system of iron, aluminium, copper, zinc in a kind of acidic mine waste water processing and the waste water.
Background technology
Metal mine acid waste water (acid mine drainage, AMD) be that sulphide ores and pyrrhotite are under air, water and microbial process, occur moltenly to soak, the series of physical chemical reactions such as oxidation, hydrolysis, form the yellowish brown acid waste water that contains plurality of heavy metal ion and sulfate anion.Generally environment has been caused at many national acidic mine waste waters and to have had a strong impact on.Pit gear and the concrete structures such as meeting corrosion pipeline, water pump, rail after acidic mine waste water is discharged; Make water acidification, consume the dissolved oxygen in the water, cause the pollution of the water bodys such as river, lake; Also can cause the pollution of agricultural land soil and cause vegetation withered, dead, crop production reduction, biological disappearance particularly consists of great threat to fish, algae, and more seriously heavy metal also can pass through the health of the direct harm humans of enrichment of food chain.
For this reason, countries in the world have been carried out a large amount of research for administering acidic mine waste water to the origin cause of formation and the improvement method of acidic mine waste water.Proposed the method for various same for treating acidic mine wastewater, such as the wetland method, but this method floor space is large, is subjected to the impact of environment also large, processes not thoroughly, and the hydrogen sulfide of effusion has pollution to environment; Such as electrochemistry, ferrite process, ion floatation method, ion-exchange resin, embrane method etc., all be feasible on these method and technologies, but cost is very high in addition, present research is main or in the laboratory or small scale wastewater treatment.
The most frequently used method of same for treating acidic mine wastewater is neutralisation traditionally: by in the chemical process and acidic substance, make metal ion form sulfide, oxyhydroxide and carbonate deposition and remove.But the quantity of slag after this method is processed is large, water ratio is high, easily causes secondary pollution, and the heavy metal ion in the waste water is just transferred in the waste residue and is not removed, they also can't be biodegradable at nature, cause chronic pollution thereby just accumulate in environment behind the entered environment.Chinese patent for example: the treatment process (application number: 201010136085.8) of mine containing sulfur minerals, As, Pb, Cd waste water, disclose a kind of by neutralization, coagulation, pH is between 8.6-9.5 in control, the precipitation removal heavy metal, make water outlet reach the method for " agricultural irrigation water quality standard ", but this technique is not carried out effective Separation and Recovery to heavy metal ions in wastewater, easily produces secondary pollution; Chinese patent and for example: the method (application number: 200910044501.9) that zinc, iron, manganese in acidic mine waste separates and reclaims, a kind of employing mechanical activation sulfurous iron ore absorption is disclosed, oxidation precipitation and neutralization precipitation same for treating acidic mine wastewater, make zinc in the waste water, iron, manganese obtains separating and the method that reclaims, but the method uses sulfurous iron ore absorption to dezincify, the sulfide precipitation composition granule is little, easily produce colloid, bring difficulty to separation, vulcanizing agent is residual in water, excessive sulphur and some heavy metal ion can generate water-soluble complexing ion and reduce treatment effect, with HCl, H
2SO
4Deng the acid contact, can produce harmful hydrogen sulfide, cause atmospheric pollution, human body is produced harm.
Summary of the invention:
Process the drawback that exists for present China metal mine acid waste water, the otherness that under different pH values, precipitates based on metal ion, the solubility product (k that reacts in conjunction with copper and zinc and sulfur-bearing organic sequestering agent
Sp) difference, adopt fractional precipitation, having developed a kind of acidic mine waste water of can eliminating pollutes, the process system of the major metal in the recoverable wastewater again, eliminated the hidden danger of waste residue secondary pollution, and recycle processing the vitriol that exists in the rear water, the water after the processing can enter the reuse of mineral processing production pond.
For realizing the object of the invention, the resource utilization recovery system of iron, aluminium, copper, zinc adopts following technical proposals in the processing of acid wastewater in mine of the present invention and the waste water:
System of the present invention is by iron removal system, be formed by connecting in turn except aluminium system, copper removal system, except Zn system, 1# settling tank, 2# settling tank, wherein the water-in of iron removal system is as the water-in of introducing the acid wastewater in mine of processing, the water outlet of described 2# settling tank enters the reuse of mineral processing production pond as the relief outlet of the clear water after processing;
Described iron removal system is comprised of iron-removing tank, solid-liquid separating machine, scum pond for recovering, at first add massfraction in the iron-removing tank and be 30% sodium hydroxide solution and regulate pH to 3.2～4, mix and blend, add again the T-301 polymeric flocculant, rapid stirring 1～3min, (speed is 60～80r/min), low rate mixing 1～5min, (speed is 40～50r/min), leaves standstill 30min.Precipitation adopts whizzer to realize solid-liquid separation in the iron-removing tank, obtains scum, and iron is realized separating and reclaimed in the waste water; Iron-removing tank water outlet and the equal overflow of separate tank water outlet are to removing the aluminium system;
The described aluminium system that removes is comprised of aluminum removing pool, thickner, aluminium slag pond for recovering, adding massfraction in the aluminum removing pool is 30% sodium hydroxide solution, pH transfers to 5～5.5, fully mix and blend adds the T-302 polymeric flocculant, rapid stirring 1～3min, (speed is 60～80r/min), low rate mixing 1～5min, (speed is 40～50r/min), leaves standstill 30min.Aluminum removing pool water outlet and concentration basin water outlet all enter the copper removal system, and wherein precipitation utilizes the suction filtration device to carry out suction filtration, realize the recovery of aluminium slag;
Described copper removal system is comprised of copper removal pond, thickner, copper ashes pond for recovering, adding massfraction in the copper removal pond is that 30% sodium hydroxide solution is regulated pH to 6.0～7.0, mix and blend, add TMS-110 metal separation agent and T-801 polymeric flocculant, rapid stirring 1～3min, (speed is 60～80r/min), low rate mixing 1～5min, (speed is 40～50r/min), leaves standstill 30min.The water outlet of copper removal pond and concentration basin water outlet all enter except Zn system, and wherein precipitation utilizes the suction filtration device to carry out suction filtration, realize the recovery of copper ashes;
The described Zn system that removes is comprised of dezincification pond, thickner, cadmia pond for recovering, adding massfraction in the dezincification pond is that 30% sodium hydroxide solution is regulated pH to 8.0～9.0, mix and blend, add the T-801 polymeric flocculant, rapid stirring 1～3min, (speed is 60～80r/min), low rate mixing 1～5min, (speed is 40～50r/min), leaves standstill 30min.The water outlet of dezincification pond and concentration basin water outlet all enter the natural settling tank of 1#, and wherein precipitation utilizes the suction filtration device to carry out suction filtration, realize the recovery of cadmia;
Remove the Zn system water outlet after the 1# settling tank precipitates 1～2 hour, supernatant liquor enters the 2# settling tank, sedimentation time: 2～3 hours, supernatant liquor entered the sodium sulfate pond for recovering, and sodium sulfate is reclaimed, and the water after the processing enters the reuse of mineral processing production pond.
In the technique scheme, described T-301 polymeric flocculant is molecular weight 1,400 ten thousand anion pp amine aqueous solutions (0.1%);
In the technique scheme, described T-302 polymeric flocculant is molecular weight 1,600 ten thousand anion pp amine aqueous solutions (0.1%);
In the technique scheme, described T-801 polymeric flocculant is molecular weight 600-1800 ten thousand nonionic polypropylene amine solution (0.1%);
In the technique scheme, the agent of described TMS-110 metal separation is sulfur-bearing organic sequestering agent (2.10%).
According to actual needs, the present invention can select to add flocculation agent accordingly in each cell process, add flocculation agent and can add a certain amount of coagulating agent before, comprises Tai-Ace S 150, aluminum chloride, ferric sulfate, iron(ic) chloride etc., accelerate settling velocity, reduce the water content of slag.
It is the effective separation that needs to reclaim metal and other metal in this unit of realization that the present invention adds TMS-110 metal separation agent purpose, improves organic efficiency, reduces subsequent operations.
Beneficial effect of the present invention:
(1) the present invention reclaims respectively four kinds of metals by the effective separation to iron, aluminium, copper, zinc, and resource has obtained effective utilization on the one hand, and the opposing party has eliminated waste residue and brought the hidden danger of secondary pollution.
(2) technique of the present invention is simple, and good waste water treatment effect is stable.
(3) processing cost of the present invention is low, and initial cost is economized, and energy consumption and working cost are low.
Description of drawings
Fig. 1 be the acidic mine waste water that proposes of the present invention process and waste water in the resource utilization recovery system schema of iron, aluminium, copper, zinc.Each label is among the figure: 1-wastewater disposal basin, 2-iron-removing tank, 3-aluminum removing pool, 4-copper removal pond, 5-dezincification pond, the 6-whizzer, 7,8,9-thickner, the 10-1# settling tank, 11-2# settling tank, 12-scum pond for recovering, 13,14,15-suction filtration device, 16-aluminium slag pond for recovering, 17-copper ashes pond for recovering, 18-cadmia pond for recovering, 19-sodium sulfate pond for recovering, 20-mineral processing production pond, 21-liquid caustic soda pond, 22-iron-removing tank medicament, 23-aluminum removing pool medicament, 24-copper removal pond medicament, 25-dezincification pond medicament.
Embodiment
For further describing the present invention, the below is take certain acid wastewater in mine as processing object, in conjunction with the accompanying drawings and embodiments iron, aluminium, copper, zinc resource recovery system in the processing of acid wastewater in mine of the present invention and the waste water is further described.
This mine wastewater pH value is 2.2, and electric conductivity is 7300 μ S/cm, and other each component and content see the following form 1:
Certain copper mine acidic mine waste water water quality situation of table 1
1, acid wastewater in mine 3000mL is by 1 wastewater disposal basin, enter 2 iron-removing tanks, regulate pH to 4 with 30% sodium hydroxide solution in the 21 liquid caustic soda ponds, mix and blend, add again T-301 polymeric flocculant 9.0mL, stirring velocity is that 70r/min stirs 1min, and stirring velocity is that 40r/min stirs 5min, leaves standstill 30min.Precipitation uses 6 whizzers to carry out solid-liquid separation, filtrate and iron-removing tank supernatant liquor enter 3 aluminum removing pools, the precipitation scum reclaims at 12 scum pond for recoverings.
2, in the aluminum removing pool except ferrous solution, transfer pH5.2 with 30% sodium hydroxide solution, mix and blend adds T-302 polymeric flocculant 7mL, stirring velocity is that 70r/min stirs 1min, stirring velocity is 40r/min stirring 5min, leaves standstill 30min.After precipitation at first adopts 7 thickners to concentrate, adopt 13 suction filtration devices to carry out suction filtration, the aluminium slag enters 16 aluminium slag pond for recoverings behind the suction filtration again, realizes the recovery of aluminium slag; Aluminum removing pool water outlet and concentration basin water outlet all enter 4 copper removal ponds.
3, in the copper removal pond, deironing, aluminum solutions are transferred pH5.6～5.8 with sodium hydroxide solution first, add 2.10%TMS-110 metal separation agent 6.0mL, abundant mix and blend, transfer pH6.0 with sodium hydroxide solution again, add T-801 polymeric flocculant 6.0mL again, stirring velocity is that 70r/min stirs 1min, be that 40r/min stirs 5min in stirring velocity again, leave standstill 30min.After precipitation at first adopts 8 thickners to concentrate, adopt 14 suction filtration devices to carry out suction filtration, copper ashes enters 17 copper ashes pond for recoverings behind the suction filtration again, realizes the recovery of copper ashes; The water outlet of copper removal pond and concentration basin water outlet all enter 5 dezincification ponds.
4, in the dezincification pond, transfer pH9.0 with sodium hydroxide solution, mix and blend leaves standstill 30min, after precipitation at first adopts 9 thickners to concentrate, adopts 15 suction filtration devices to carry out suction filtration again, and cadmia enters 18 cadmia pond for recoverings behind the suction filtration, realizes the recovery of cadmia; The water outlet of dezincification pond and concentration basin water outlet all enter the 10-1# settling tank.
5, after precipitation reuse of water outlet.The water outlet of dezincification pond and press filtration water are after the 1# settling tank leaves standstill 2 hours, and supernatant liquor enters the 11-2# settling tank, continue to leave standstill 2 hours, and supernatant liquor enters 19 sodium sulfate pond for recoverings, and sodium sulfate is reclaimed, and water outlet enters 20 mineral processing production pond reuses.
The content of iron, aluminium, copper and zinc is respectively 39.72%, 17.13%, 15.71% and 33.64% in iron, aluminium, copper and the cadmia that reclaims after measured, and the rate of recovery reaches respectively 97.6%, 94.2%, 45.7% and 64.4%.
Embodiment 2
1, acid wastewater in mine 3000mL is by 1 wastewater disposal basin, enter 2 iron-removing tanks, regulate pH to 3.8 with 30% sodium hydroxide solution in the 21 liquid caustic soda ponds, mix and blend, add again T-301 polymeric flocculant 9.0mL, stirring velocity is that 65r/min stirs 1min, and stirring velocity is that 45r/min stirs 5min, leaves standstill 30min.Precipitation uses 6 whizzers to carry out solid-liquid separation, filtrate and iron-removing tank supernatant liquor enter 3 aluminum removing pools, the precipitation scum reclaims at 12 scum pond for recoverings.
2, in the aluminum removing pool except ferrous solution, transfer pH5.6 with 30% sodium hydroxide solution, fully mix and blend adds T-801 polymeric flocculant 6mL again, stirring velocity is that 65r/min stirs 1min, stirring velocity is 45r/min stirring 5min, leaves standstill 30min.After precipitation at first adopts 7 thickners to concentrate, adopt 13 suction filtration devices to carry out suction filtration, the aluminium slag enters 16 aluminium slag pond for recoverings behind the suction filtration again, realizes the recovery of aluminium slag; Aluminum removing pool water outlet and concentration basin water outlet all enter 4 copper removal ponds.
3, in the copper removal pond, deironing, aluminum solutions are transferred pH6.0～6.2 with sodium hydroxide solution first, add 2.10%TMS-110 metal separation agent 5.2mL, abundant mix and blend, transfer pH6.5 with sodium hydroxide solution again, add T-801 polymeric flocculant 6.0mL again, stirring velocity is that 70r/min stirs 1min, stirring velocity is that 40r/min stirs 5min, leaves standstill 30min.After precipitation at first adopts 8 thickners to concentrate, adopt 14 suction filtration devices to carry out suction filtration, copper ashes enters 17 copper ashes pond for recoverings behind the suction filtration again, realizes the recovery of copper ashes; The water outlet of copper removal pond and concentration basin water outlet all enter 5 dezincification ponds.
4, in the dezincification pond, transfer pH9.0 with sodium hydroxide solution, mix and blend leaves standstill 30min,, after precipitation at first adopts 9 thickners to concentrate, adopt again 15 suction filtration devices to carry out suction filtration, cadmia enters 18 cadmia pond for recoverings behind the suction filtration, realizes the recovery of cadmia; The water outlet of dezincification pond and concentration basin water outlet all enter the 10-1# settling tank.
5, after precipitation reuse of water outlet.The water outlet of dezincification pond and press filtration water are after the 1# settling tank leaves standstill 2 hours, and supernatant liquor enters the 11-2# settling tank, continue to leave standstill 3 hours, and supernatant liquor enters 19 sodium sulfate pond for recoverings, and sodium sulfate is reclaimed, and water outlet enters 20 mineral processing production pond reuses.
The content of iron, aluminium, copper and zinc is respectively 37.83%, 17.58%, 16.52% and 34.43% in iron, aluminium, copper and the cadmia that reclaims after measured, and the rate of recovery reaches respectively 92.5%, 99.2%, 55.7% and 65.8%.
Claims (1)
- An acidic mine waste water process and waste water in the resource utilization recovery system of iron, aluminium, copper, zinc, it is characterized in that: this system is by iron removal system, be formed by connecting in turn except aluminium system, copper removal system, except Zn system, 1# settling tank, 2# settling tank, wherein the water-in of iron removal system is as the water-in of introducing the acid wastewater in mine of processing, the water outlet of described 2# settling tank enters the reuse of mineral processing production pond as the relief outlet of the clear water after processing;Described iron removal system is comprised of iron-removing tank, solid-liquid separating machine, scum pond for recovering, at first add 30% sodium hydroxide solution in the iron-removing tank and regulate pH to 3.2～4, mix and blend, add again the T-301 polymeric flocculant, rapid stirring 1～3min, low rate mixing 1～5min leaves standstill 30min, precipitation adopts the high efficiency separation machine to realize solid-liquid separation in the iron-removing tank, and iron-removing tank water outlet and the equal overflow of solid-liquid separating machine water outlet are to removing the aluminium system;The described aluminium system that removes is comprised of aluminum removing pool, thickner, aluminium slag pond for recovering, in aluminum removing pool, add 30% sodium hydroxide solution, pH transfers to 5～5.5, fully mix and blend adds the T-302 polymeric flocculant, rapid stirring 1～3min, low rate mixing 1～5min, leave standstill 30min, aluminum removing pool water outlet and thickner water outlet all enter the copper removal system, and wherein precipitation adopts the suction filtration device to carry out suction filtration;Described copper removal system is comprised of copper removal pond, thickner, copper ashes pond for recovering, in the copper removal pond, add 30% sodium hydroxide solution adjusting pH to 6.0～7.0, mix and blend, add TMS-110 metal separation agent and T-801 polymeric flocculant, rapid stirring 1～3min, low rate mixing 1～5min leaves standstill 30min, the water outlet of copper removal pond and thickner water outlet all enter except Zn system, and wherein precipitation adopts the suction filtration device to carry out suction filtration;The described Zn system that removes is comprised of dezincification pond, thickner, cadmia pond for recovering, in the dezincification pond, add 30% sodium hydroxide solution adjusting pH to 8.0～9.0, mix and blend, add TMS-110 metal separation agent and T-801 polymeric flocculant, rapid stirring 1～3min, low rate mixing 1～5min leaves standstill 30min, the water outlet of dezincification pond and thickner water outlet all enter the 1# settling tank, and wherein precipitation adopts the suction filtration device to carry out suction filtration;Remove the Zn system water outlet after the 1# settling tank precipitates 1～2 hour, supernatant liquor enters the 2# settling tank, sedimentation time: 2～3 hours, supernatant liquor entered the sodium sulfate pond for recovering, and water outlet enters the reuse of mineral processing production pond;Described T-301 polymeric flocculant is that molecular weight 1,400 ten thousand, mass percent concentration are 0.1% anionic polyacrylamide solution;Described T-302 polymeric flocculant is that molecular weight 1,600 ten thousand, mass percent concentration are 0.1% anionic polyacrylamide solution;Described T-801 polymeric flocculant is that molecular weight 600-1800 ten thousand, mass percent concentration are 0.1% non-ionic polyacrylamide solution;The agent of described TMS-110 metal separation is that mass percent concentration is 2.1% sulfur-bearing organic sequestering agent.
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| CN102583836A (en) * | 2012-03-15 | 2012-07-18 | 南京银茂铅锌矿业有限公司 | Method for treating copper/lead/zinc ore mining sewage |
| CN103214121B (en) * | 2013-04-27 | 2014-12-24 | 福建格林锘贝尔环保科技有限公司 | Method for recycling copper and iron in acid mine wastewater by high-polymer chelating-precipitating agent two-step process |
| CN104671565B (en) * | 2015-01-19 | 2017-01-11 | 浙江博世华环保科技有限公司 | Treatment method of industrial refuse landfill percolate |
| CN104876369A (en) * | 2015-06-09 | 2015-09-02 | 长春黄金研究院 | Comprehensive treatment process of acid wastewater of nonferrous metal mine |
| CN107365910A (en) * | 2016-05-13 | 2017-11-21 | 浙江蓝天环保高科技股份有限公司 | A kind of method of the purifying containing zinc ion and copper ion organic liquid waste |
| CN105858969A (en) * | 2016-06-07 | 2016-08-17 | 韶关市雅鲁环保实业有限公司 | Wastewater treatment process of iron-copper-sulfur polymetallic mine slurry detention reservoir |
| CN107029892B (en) * | 2017-03-22 | 2019-08-02 | 江西理工大学 | A kind of method that copper flash clinker settles microfine Pb-Zn tailings as flocculant |
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| CN107162302A (en) * | 2017-06-20 | 2017-09-15 | 临涣焦化股份有限公司 | It is a kind of that chimney can be condensed to the method that Sewage treatment is utilized |
| CN114436426A (en) * | 2020-11-06 | 2022-05-06 | 湖南天童环保有限公司 | Treatment agent and process for metallurgical waste acid and metal and heavy metal-containing composite wastewater |
| CN112537856B (en) * | 2020-11-16 | 2023-12-29 | 武汉理工大学 | Method for treating acid mine wastewater containing heavy metal ions |
| CN112645493A (en) * | 2020-12-22 | 2021-04-13 | 高博 | Iron pollutant recovery device for casting cooling wastewater |
| CN114014462A (en) * | 2021-11-03 | 2022-02-08 | 河北驰田环保科技有限公司 | Low-cost treatment method for recycling metal ions in acidic mine water |
| CN115259488A (en) * | 2022-08-04 | 2022-11-01 | 成都美富特环保产业集团有限公司 | Treatment system and treatment method for acidic copper-containing wastewater |
| CN115385473B (en) * | 2022-08-11 | 2024-01-16 | 广东工业大学 | Method for recovering valuable metals in acid mine wastewater |
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| EP1772432A4 (en) * | 2004-03-05 | 2011-09-07 | Hosoda Electric Co Ltd | Acidic water producing device, acidic water producing method, and acidic water |
| US20070045189A1 (en) * | 2005-08-31 | 2007-03-01 | General Electric Company | Acid mine water demineralization methods |
| CN101219844B (en) * | 2008-01-23 | 2010-08-11 | 太原理工大学 | Technique for biological treatment of mine acidic wastewater |
| CN101402491A (en) * | 2008-10-27 | 2009-04-08 | 合肥工业大学 | Method for treating heavy metal-containing acidic waste water and recycling heavy metal with biomass fixed bed |
| CN101628773B (en) * | 2009-08-04 | 2011-04-20 | 紫金矿业集团股份有限公司 | Treatment process of copper-iron-contained high-concentration acidic mine wastewater |
| CN102079594B (en) * | 2010-12-15 | 2012-01-04 | 东华大学 | Treatment method of mine wastewater |
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